Simulation of a sorbent enhanced gasification pilot reactor and validation of reactor model

被引:17
作者
Pitkaoja, Antti [1 ]
Ritvanen, Jouni [1 ]
Hafner, Selina [2 ]
Hyppanen, Timo [1 ]
Scheffknecht, Gunter [2 ]
机构
[1] Lappeenranta Lahti Univ Technol, LUT Sch Energy Syst, POB 20, FI-53851 Lappeenranta, Finland
[2] Univ Stuttgart, Inst Combust & Power Plant Technol IFK, Pfaffenwaldring 23, D-70569 Stuttgart, Germany
基金
芬兰科学院; 欧盟地平线“2020”;
关键词
Sorbent enhanced gasification; Gasification; Biomass thermochemical conversion; Simulation; Limestone; Hydrodynamics; DUAL FLUIDIZED-BED; BIOMASS GASIFICATION; MATHEMATICAL-MODEL; CO2; COMBUSTION; BUBBLE; KINETICS; CHAR; COAL; CONVERSION;
D O I
10.1016/j.enconman.2019.112318
中图分类号
O414.1 [热力学];
学科分类号
摘要
Sorption enhanced gasification (SEG) is a promising technology for production of a renewable feedstock gas for biofuel synthesis processes. The technology has been previously demonstrated at pilot scale. Scaling of the technology to an industrial size requires knowledge from governing phenomena. One-dimensional bubbling fluidized bed (BFB) reactor model was developed and validated against experimental data from 200kW(th) dual fluidized bed facility. Sub-models for biomass gasification, reactive bed material and fluidized bed hydrodynamics were incorporated into the model frame. The model gave satisfactory predictions for bed material conversion, temperature profiles and gas composition of the producer gas. The conducted validation improved understanding of bed material conversion, water-gas shift reaction and hydrodynamics and their role in SEG reactors. Further refinement and comprehensive validation of the model with additional data from the pilot is required. The knowledge from the comprehensive validation can be utilized in simulation of an industrial size reactor.
引用
收藏
页数:14
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